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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
31
Benzene
71-43-2
C
6
H
6
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
2187
Methyldiethanolamine (MDEA)
105-59-9
C
5
H
1
3
NO
2
Overview
Details
Search for mixtures containing this mixture as subsystem
Search data for binary subsystems
Mixture Data
Databank
Sets
Points
Temperature
Range
Pressure
Range
Vapor-Liquid Equilibria
VLE
73
472
278-473 K
7-103421 kPa
174
1050
1051
41
174
1050
1051
2187
7
174
1050
2187
22
174
1051
2187
3
Heats of Mixing
HE
21
176
300-400 K
1380-6900 kPa
174
1050
1051
2187
21
Gas Solubilities
GLE
335
2452
283-473 K
0-20000 kPa
174
1050
2187
323
174
1051
2187
12
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
64
436
288-618 K
348-304070 kPa
31
174
1050
59
31
174
2187
4
174
1050
1051
1
Heat Capacities of Mixtures, Excess Heat Capacities
CPE
4
39
298 K (const.)
n.a.
174
1050
2187
4
Densities and Volumes of Mixtures, Excess Volumes
VE
16
108
298-423 K
101-808 kPa
174
1050
2187
16
Critical Data of Mixtures
CRI
1
7
288-304 K
7615-8268 kPa
174
1050
1051
1
Mixture Viscosities
VIS
25
206
293-382 K
n.a.
174
1050
2187
25
Mixture Surface Tensions
MSFT
46
461
288-423 K
97-33791 kPa
174
1050
1051
37
174
1050
2187
8
174
1051
2187
1
Mixture P-v-T Data
MPVT
20
836
293-618 K
5-304070 kPa
31
174
1050
2
174
1050
2187
18
Gas Hydrate Data
GHD
89
733
189-294 K
1100-40000 kPa
31
174
1050
1
31
174
1051
6
174
1050
1051
76
174
1051
2187
6
Diffusion Coefficients
DIF
6
48
288-323 K
n.a.
174
1050
2187
6
Further Thermodynamic Properties
X
220
10404
243-648 K
2-27710 kPa
31
174
1050
1051
2187
1
31
174
1050
2187
2
31
174
2187
2
174
1050
1051
19
174
1050
1051
2187
7
174
1050
2187
187
174
1051
2187
2
Total
920
16378
31
174
1050
62
31
174
1050
1051
2187
1
31
174
1050
2187
2
31
174
1051
6
31
174
2187
6
174
1050
1051
175
174
1050
1051
2187
35
174
1050
2187
609
174
1051
2187
24
Dortmund Data Bank Version: February 2024
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